US1539342A - Adsorbent material and the manufacture and application thereof - Google Patents
Adsorbent material and the manufacture and application thereof Download PDFInfo
- Publication number
- US1539342A US1539342A US679499A US67949923A US1539342A US 1539342 A US1539342 A US 1539342A US 679499 A US679499 A US 679499A US 67949923 A US67949923 A US 67949923A US 1539342 A US1539342 A US 1539342A
- Authority
- US
- United States
- Prior art keywords
- gel
- application
- manufacture
- alkali metal
- adsorbent material
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000003463 adsorbent Substances 0.000 title description 5
- 238000004519 manufacturing process Methods 0.000 title description 4
- 239000000463 material Substances 0.000 title description 4
- 239000000499 gel Substances 0.000 description 17
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 9
- -1 alkali metal salts Chemical class 0.000 description 9
- 229910052783 alkali metal Inorganic materials 0.000 description 8
- 230000000274 adsorptive effect Effects 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 7
- 239000000741 silica gel Substances 0.000 description 6
- 229910002027 silica gel Inorganic materials 0.000 description 6
- 239000007789 gas Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000000470 constituent Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 206010001497 Agitation Diseases 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 150000001339 alkali metal compounds Chemical class 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000011335 coal coke Substances 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 150000003377 silicon compounds Chemical class 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- FDNAPBUWERUEDA-UHFFFAOYSA-N silicon tetrachloride Chemical compound Cl[Si](Cl)(Cl)Cl FDNAPBUWERUEDA-UHFFFAOYSA-N 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L sodium sulphate Substances [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- DWFFKGPZNGKUPH-UHFFFAOYSA-N sulfanylidenesilicon Chemical compound S=[Si] DWFFKGPZNGKUPH-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
- C01B33/152—Preparation of hydrogels
Definitions
- This invention relates to an improvement in adsorbent materials and in the manufacture and application thereof.
- silica can be obtained in the gel form e. g. by treating sodium silicate solutions with acid, washing with water with or without dialysis and drying the washed gel at ordinary temperature in vacuo or at a raised temperature- Such a dried gel is known to possess powerful adsorbent properties and it has been proposed to use it for separating the various constituents of gases or liquids.
- the invention further includes the separation of constituents from fluids e. g. liquids or gases, by the aid of silica gel containing practically no alkali metal salts and the revivification of the gel by heating to a high temperature.
- the invention specifically includes one method of obtaining such a gel, namely by the hydrolysis of silicon compounds in ab- 50. sence of soluble and non-volatile bases, but the gel free from alkali metal salts and 'possesing the desirable property already Application flied December 8, 1923. Serial No. 679,499.
- Silicon chloride is poured into water with.
- the gel is washed and then carefully dried at 100 C. with heat though it may be dried direct (without washing) if desired, thus the drying may last 12-24hours; the temperature may then be slowly raised to 400 C.
- the product is practically free from alkali metal salts such as, sodium chloride or sulphate. Traces of such salts are undesirable since they tend to accelerate crystallization of the amorphous silica. -Hence the gel obtained by my process can be heated to a higher temperature without destroying its adsorptive properties e. g. up to 900 to 1000 C.
- Silica gel free from alkali metal salts can be used for adsorbing constituents from a liquid or a gas and I find that in treating coal gas or coke oven gas' the silica gel is contaminated by tar, or polymerized'products e. g. of dio'lefinic nature and thus it must be revivified by heating in an oxidizing atmosphere.
- the gel produced according to my invention is particularly valuable for-treating such gases since I can revivify it by heating to a temperature sufiicient to burn oil. such polymerized bodies without seriously affecting the adsorptive properties. Silicon sulphide or various silicon halogen compounds can also be used as raw materials.
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
Patented May 26, 1925.
,aaz
EVAN c. WILLIA S, or
I ADSORBENT MATERIAL AND THE MANUFACTURE AND APPLICATION THEREOF.
1T0 Drawing.
To all whom it concerm: Be it known that I, EVAN CLIFFORD WIL- LIAMs, a subject of the King ofGreat Britain, residing at Huddersfield, inthe county 5 of York and Kingdom of England, have invented certain new and useful Improvements in Adsorbent, Materials and the Manufacture and Application Thereof, of which the following is a specification.
This invention relates to an improvement in adsorbent materials and in the manufacture and application thereof.
g It is known that silica can be obtained in the gel form e. g. by treating sodium silicate solutions with acid, washing with water with or without dialysis and drying the washed gel at ordinary temperature in vacuo or at a raised temperature- Such a dried gel is known to possess powerful adsorbent properties and it has been proposed to use it for separating the various constituents of gases or liquids.
' When such a gel is prepared according to known methods, even after prolonged washing with water, it is found that on heating to a temperature of say 900 C. the adsorptive properties of the gel are materially reduced. It is one object of my invention to overcome this disadvantage since 3 vigorous heating of the gel is most desirable for purposes of revivification.
I have discovered that a gel which is practically free from alkali metal salts can be so heated to say 900 C. with safety.
Apparently the traces of alkali metal salts present in gels hitherto prepared are capable of causing some catalytic acceleration of the crystallization of the silica gel on heating and this effect is enormously reduced in absence of alkali metal salts.
The invention further includes the separation of constituents from fluids e. g. liquids or gases, by the aid of silica gel containing practically no alkali metal salts and the revivification of the gel by heating to a high temperature.
The invention specifically includes one method of obtaining such a gel, namely by the hydrolysis of silicon compounds in ab- 50. sence of soluble and non-volatile bases, but the gel free from alkali metal salts and 'possesing the desirable property already Application flied December 8, 1923. Serial No. 679,499.
mentioned is considered to be a broadly novel product.
Example.
Silicon chloride is poured into water with.
The gel is washed and then carefully dried at 100 C. with heat though it may be dried direct (without washing) if desired, thus the drying may last 12-24hours; the temperature may then be slowly raised to 400 C.
Care is taken not to destroy the microstructure of the gel and thus to afl'ect its adsorptive properties.
The product is practically free from alkali metal salts such as, sodium chloride or sulphate. Traces of such salts are undesirable since they tend to accelerate crystallization of the amorphous silica. -Hence the gel obtained by my process can be heated to a higher temperature without destroying its adsorptive properties e. g. up to 900 to 1000 C.
Silica gel free from alkali metal salts (whether prepared as above described or in other manner) can be used for adsorbing constituents from a liquid or a gas and I find that in treating coal gas or coke oven gas' the silica gel is contaminated by tar, or polymerized'products e. g. of dio'lefinic nature and thus it must be revivified by heating in an oxidizing atmosphere. The gel produced according to my invention is particularly valuable for-treating such gases since I can revivify it by heating to a temperature sufiicient to burn oil. such polymerized bodies without seriously affecting the adsorptive properties. Silicon sulphide or various silicon halogen compounds can also be used as raw materials.
I declare that what I claim is T1. Adsorptive silica gel free from alkali metal salts.
2. Adsorptive silica gel so free from alkali metal compounds. that it can be repeatedly heated to about 900 C. without In witness whereof, I have hereunto substantial diminution of its adsorptive' signed my name this 22 day. of November powers. 1923, in the presence of two subscribing 5 1611 process of producing dryhlsiliga. witnesses.
e w 0 com rises mlxm s1 mm c on e vith water wit h such agita tion and in such WILLIAMS proportions that a. gel is obtained on stand- Witnesses:
mg and then drymg said gel slowly by HAROLD E. Po'rrs,
heating. v E'. DREW BARTLM'I.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US679499A US1539342A (en) | 1923-12-08 | 1923-12-08 | Adsorbent material and the manufacture and application thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US679499A US1539342A (en) | 1923-12-08 | 1923-12-08 | Adsorbent material and the manufacture and application thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1539342A true US1539342A (en) | 1925-05-26 |
Family
ID=24727150
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US679499A Expired - Lifetime US1539342A (en) | 1923-12-08 | 1923-12-08 | Adsorbent material and the manufacture and application thereof |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1539342A (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2594725A (en) * | 1948-01-06 | 1952-04-29 | Herbert E Britt | Method of producing artificial snow |
| US2772984A (en) * | 1952-07-12 | 1956-12-04 | Allied Chem & Dye Corp | Pigment |
| US2794002A (en) * | 1953-12-14 | 1957-05-28 | Universal Oil Prod Co | Method for producing solid siliceous catalyst |
| US2798792A (en) * | 1949-07-20 | 1957-07-09 | Helsingborgs Gummifabriks | Method for the production of finely divided silicon dioxide |
| US2810455A (en) * | 1955-10-17 | 1957-10-22 | Grace W R & Co | Method of dehydrating gases |
| US2965448A (en) * | 1954-08-31 | 1960-12-20 | Du Pont | A new crystalline form of silica and its preparation |
| US3125043A (en) * | 1964-03-17 | Method of removing volatile constituents | ||
| US3180760A (en) * | 1960-03-05 | 1965-04-27 | Marc Inc | Method of producing secondary dry cells with lead electrodes and sulfuric acid electrolyte |
| US3272434A (en) * | 1963-06-03 | 1966-09-13 | Albert C Zettlemoyer | Nucleating process |
| US4626422A (en) * | 1985-06-24 | 1986-12-02 | Gte Products Corporation | High purity high surface area silicon nitride |
| US4710368A (en) * | 1985-06-24 | 1987-12-01 | Gte Products Corporation | High purity high surface area alpha crystalline silicon nitride |
| US5158758A (en) * | 1989-04-24 | 1992-10-27 | International Minerals & Chemical Corp. | Production of silica having high specific surface area |
-
1923
- 1923-12-08 US US679499A patent/US1539342A/en not_active Expired - Lifetime
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3125043A (en) * | 1964-03-17 | Method of removing volatile constituents | ||
| US2594725A (en) * | 1948-01-06 | 1952-04-29 | Herbert E Britt | Method of producing artificial snow |
| US2798792A (en) * | 1949-07-20 | 1957-07-09 | Helsingborgs Gummifabriks | Method for the production of finely divided silicon dioxide |
| US2772984A (en) * | 1952-07-12 | 1956-12-04 | Allied Chem & Dye Corp | Pigment |
| US2794002A (en) * | 1953-12-14 | 1957-05-28 | Universal Oil Prod Co | Method for producing solid siliceous catalyst |
| US2965448A (en) * | 1954-08-31 | 1960-12-20 | Du Pont | A new crystalline form of silica and its preparation |
| US2810455A (en) * | 1955-10-17 | 1957-10-22 | Grace W R & Co | Method of dehydrating gases |
| US3180760A (en) * | 1960-03-05 | 1965-04-27 | Marc Inc | Method of producing secondary dry cells with lead electrodes and sulfuric acid electrolyte |
| US3272434A (en) * | 1963-06-03 | 1966-09-13 | Albert C Zettlemoyer | Nucleating process |
| US4626422A (en) * | 1985-06-24 | 1986-12-02 | Gte Products Corporation | High purity high surface area silicon nitride |
| US4710368A (en) * | 1985-06-24 | 1987-12-01 | Gte Products Corporation | High purity high surface area alpha crystalline silicon nitride |
| US5158758A (en) * | 1989-04-24 | 1992-10-27 | International Minerals & Chemical Corp. | Production of silica having high specific surface area |
| US5861110A (en) * | 1989-04-24 | 1999-01-19 | Chieng; Paul C. | Silica having high specific surface area and a narrow pore distribution |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US1539342A (en) | Adsorbent material and the manufacture and application thereof | |
| US1506118A (en) | Method of preparing siliceous material | |
| US1540446A (en) | Aluminum gellike absorbent and process for making same | |
| US2206021A (en) | Catalytic cracking and cracking catalysts | |
| US1555639A (en) | Filtering material and process of preparing the same | |
| US1882146A (en) | Removal of sulphur from gasoline or the like | |
| US1079899A (en) | Purifying alumina. | |
| US1507105A (en) | Process of oxidizing hydrogen sulphide | |
| US1393225A (en) | And walter l | |
| US1618149A (en) | Absorbent decolorizing medium | |
| US551941A (en) | And josiah ii | |
| US961651A (en) | Method of producing acid and fire proof bodies. | |
| US1262770A (en) | Absorbent material and process of producing the same. | |
| GB263199A (en) | An improved process for the production of active silica gels with fine capillary pores | |
| GB266133A (en) | Improvements in the manufacture and production of highly active silica gels | |
| US1419463A (en) | Process of purifying sodium carbonate and the like | |
| SU51043A1 (en) | Method for producing silica gel from nepheline | |
| GB370950A (en) | Tile and method of making the same | |
| US1194015A (en) | Method of xtreating | |
| US1562001A (en) | Method of treating oil | |
| GB184206A (en) | Improved process of manufacturing soluble phosphates | |
| US1917686A (en) | Recovery of sulphur | |
| US1429932A (en) | Process for the chlorination of montan wax | |
| GB183443A (en) | Improved process of purifying sulphate of baryta, or other mineral substances | |
| GB146956A (en) | Production of alcohols, esters and the like from still gases of petroleum |